jeap
Chemical
- Nov 1, 2006
- 36
Hi all!
I'm trying to dimension a vacuum deoxygen column to pretreat 170 m3/h of river water to be injected in an oilfield. The oxygen and other dissolved gases are removed from water by means of vacuum generated with a liquid ring pump. The process is carried out at 25ºC and 35 mmHg (abs).
However, since this is a vacuum process I'm not sure if the gas/vapour flowrate I considered is ok. I took into account dissolved gases plus water vapor in a flowrate of 50 sm3/d (from an existing process with this pump capacity).
I've followed recommendations and procedures to dimension packed towers in the usual manner. Dimensions I obtained at first seem to be right. (1.2 m diameter, 3 m packing height, HDPE pall rings 1")
Do you have some advice?
And some details on the internals design also be welcome.
Thanks in advance.
I'm trying to dimension a vacuum deoxygen column to pretreat 170 m3/h of river water to be injected in an oilfield. The oxygen and other dissolved gases are removed from water by means of vacuum generated with a liquid ring pump. The process is carried out at 25ºC and 35 mmHg (abs).
However, since this is a vacuum process I'm not sure if the gas/vapour flowrate I considered is ok. I took into account dissolved gases plus water vapor in a flowrate of 50 sm3/d (from an existing process with this pump capacity).
I've followed recommendations and procedures to dimension packed towers in the usual manner. Dimensions I obtained at first seem to be right. (1.2 m diameter, 3 m packing height, HDPE pall rings 1")
Do you have some advice?
And some details on the internals design also be welcome.
Thanks in advance.